BR112012024193A2 - starting method for fractionator - Google Patents

starting method for fractionator

Info

Publication number
BR112012024193A2
BR112012024193A2 BR112012024193A BR112012024193A BR112012024193A2 BR 112012024193 A2 BR112012024193 A2 BR 112012024193A2 BR 112012024193 A BR112012024193 A BR 112012024193A BR 112012024193 A BR112012024193 A BR 112012024193A BR 112012024193 A2 BR112012024193 A2 BR 112012024193A2
Authority
BR
Brazil
Prior art keywords
fractionator
starting method
preheating
wax fraction
hydrocracking
Prior art date
Application number
BR112012024193A
Other languages
Portuguese (pt)
Other versions
BR112012024193B1 (en
Inventor
Kazuhiko Tasaka
Original Assignee
Cosmo Oil Co Ltd
Inpex Corp
Japan Petroleum Exploration Co
Jx Nippon Oil & Energy Coporation
Japan Oil Gas & Metals Jogmec
Nippon Steel Eng Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=44672999&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=BR112012024193(A2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority claimed from JP2010070287A external-priority patent/JP5599633B2/en
Priority claimed from JP2010076987A external-priority patent/JP5599634B2/en
Application filed by Cosmo Oil Co Ltd, Inpex Corp, Japan Petroleum Exploration Co, Jx Nippon Oil & Energy Coporation, Japan Oil Gas & Metals Jogmec, Nippon Steel Eng Co Ltd filed Critical Cosmo Oil Co Ltd
Publication of BR112012024193A2 publication Critical patent/BR112012024193A2/en
Publication of BR112012024193B1 publication Critical patent/BR112012024193B1/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G7/00—Distillation of hydrocarbon oils
    • C10G7/12—Controlling or regulating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/42—Regulation; Control
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/14—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural parallel stages only
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G7/00—Distillation of hydrocarbon oils
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1022—Fischer-Tropsch products
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4031—Start up or shut down operations
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4081—Recycling aspects

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

método de partida para fracionador. a presente invenção refere-se a um método de partida para um fracionador que é suprido com, e destila fracionariamente, um produto hidrocraqueado obtido em uma etapa de hidrocraqueamento de fração de cera hidrocraqueando uma fração de cera co ntida em um óleo sintético de fischer-tropsch, o método incluindo uma etapa de preaquecimento de preaquecer o fracionador usando um óleo de hidrocarboneto que inclui pelo menos uma porção do produto hidrocraqueado e é líquido a temperatura normal e pressão normal.Starting method for fractionator. The present invention relates to a starting method for a fractionator which is supplied with, and fractionally distilled, a hydrocracked product obtained in a wax fraction hydrocracking step by hydrocracking a wax fraction contained in a synthetic fischer-oil. tropsch, the method including a preheating step of preheating the fractionator using a hydrocarbon oil that includes at least a portion of the hydrocracked product and is liquid at normal temperature and normal pressure.

BR112012024193A 2010-03-25 2011-03-15 starting method for fractionator BR112012024193B1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2010070287A JP5599633B2 (en) 2010-03-25 2010-03-25 Rectification tower startup method
JP2010076987A JP5599634B2 (en) 2010-03-30 2010-03-30 Rectification tower startup method
PCT/JP2011/055992 WO2011118442A1 (en) 2010-03-25 2011-03-15 Rectifying column start-up method

Publications (2)

Publication Number Publication Date
BR112012024193A2 true BR112012024193A2 (en) 2016-07-05
BR112012024193B1 BR112012024193B1 (en) 2018-10-09

Family

ID=44672999

Family Applications (1)

Application Number Title Priority Date Filing Date
BR112012024193A BR112012024193B1 (en) 2010-03-25 2011-03-15 starting method for fractionator

Country Status (9)

Country Link
US (1) US9404050B2 (en)
EP (1) EP2551330B2 (en)
CN (1) CN102858920B (en)
AU (1) AU2011230766B2 (en)
BR (1) BR112012024193B1 (en)
CA (1) CA2794475C (en)
EA (1) EA024240B1 (en)
MY (1) MY161900A (en)
WO (1) WO2011118442A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6008534B2 (en) 2012-03-28 2016-10-19 独立行政法人石油天然ガス・金属鉱物資源機構 Method for producing diesel fuel or diesel fuel substrate

Family Cites Families (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2939293A (en) * 1958-04-07 1960-06-07 Phillips Petroleum Co Start-up procedure-gas fractionator
US3873440A (en) * 1973-11-14 1975-03-25 Universal Oil Prod Co Startup method for exothermic catalytic reaction zones
US4127392A (en) * 1977-02-27 1978-11-28 Conoco Methanation Company Methanation process start-up
JPS60220104A (en) * 1984-04-18 1985-11-02 Asia Sekiyu Kk Automatic startup of distillation plant operation
JPH06158059A (en) * 1992-11-17 1994-06-07 Cosmo Oil Co Ltd Method for start-up of fractionator
US6583186B2 (en) 2001-04-04 2003-06-24 Chevron U.S.A. Inc. Method for upgrading Fischer-Tropsch wax using split-feed hydrocracking/hydrotreating
JP3834501B2 (en) * 2001-11-01 2006-10-18 住友化学株式会社 Distillation tower and start-up method of distillation tower
GB2401112C (en) * 2002-02-13 2007-01-16 Sasol Technology Process for starting up a fischer-tropsch reactor
JP3945773B2 (en) 2003-04-23 2007-07-18 株式会社ジャパンエナジー Eco-friendly fuel oil and its manufacturing method
US6958364B1 (en) * 2004-07-15 2005-10-25 Chevron U.S.A. Inc. Use of Fischer-Tropsch condensate as a lean oil for heavy ends recovery from Fischer-Tropsch tail gas
RU2414445C2 (en) * 2005-12-09 2011-03-20 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Method of starting process for producing hydrocarbons from synthetic gas
MY145762A (en) * 2005-12-09 2012-04-13 Shell Int Research Method to start a process for producing hydrocarbons from synthesis gas
WO2007069197A2 (en) 2005-12-15 2007-06-21 Sasol Technology (Proprietary) Limited Production of hydrocarbons from natural gas
RU2415904C2 (en) * 2006-03-30 2011-04-10 Ниппон Стил Инджиниринг Ко., Лтд. System of liquid fuel synthesis
JPWO2007114276A1 (en) 2006-03-30 2009-08-13 新日鉄エンジニアリング株式会社 Method for starting liquid fuel synthesis system and liquid fuel synthesis system
DE102006039191A1 (en) * 2006-08-21 2008-03-20 Wacker Chemie Ag Continuous production of organosilanes
JP5174411B2 (en) * 2007-09-28 2013-04-03 独立行政法人石油天然ガス・金属鉱物資源機構 Effective heat utilization method of tube reformer
JP5752870B2 (en) * 2008-03-14 2015-07-22 独立行政法人石油天然ガス・金属鉱物資源機構 Operation method of hydrotreating equipment
JP2010070287A (en) 2008-09-17 2010-04-02 Canon Inc Paper sheet stacking device and recording device
JP5610684B2 (en) 2008-09-26 2014-10-22 キヤノン株式会社 Optical glass and optical element
JP5296478B2 (en) 2008-09-30 2013-09-25 Ｊｘ日鉱日石エネルギー株式会社 Rectification tower startup method
JP5296477B2 (en) * 2008-09-30 2013-09-25 Ｊｘ日鉱日石エネルギー株式会社 Startup method of naphtha distillate hydrotreating reactor
US7985777B2 (en) * 2008-10-30 2011-07-26 Stickney Michael J Systems and methods for reactive distillation with recirculation of light components

Also Published As

Publication number Publication date
EA201290912A1 (en) 2013-03-29
US9404050B2 (en) 2016-08-02
AU2011230766A1 (en) 2012-11-08
EP2551330B2 (en) 2019-01-23
CA2794475A1 (en) 2011-09-29
BR112012024193B1 (en) 2018-10-09
EP2551330A4 (en) 2014-03-05
EP2551330B1 (en) 2015-10-28
EA024240B1 (en) 2016-08-31
MY161900A (en) 2017-05-15
WO2011118442A1 (en) 2011-09-29
CN102858920B (en) 2017-07-11
EP2551330A1 (en) 2013-01-30
AU2011230766B2 (en) 2013-11-28
CA2794475C (en) 2015-10-20
US20130175010A1 (en) 2013-07-11
CN102858920A (en) 2013-01-02

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Legal Events

Date Code Title Description
B06A Patent application procedure suspended [chapter 6.1 patent gazette]
B09A Decision: intention to grant [chapter 9.1 patent gazette]
B16A Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]

Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 15/03/2011, OBSERVADAS AS CONDICOES LEGAIS.

B21F Lapse acc. art. 78, item iv - on non-payment of the annual fees in time

Free format text: REFERENTE A 13A ANUIDADE.

B24J Lapse because of non-payment of annual fees (definitively: art 78 iv lpi, resolution 113/2013 art. 12)

Free format text: EM VIRTUDE DA EXTINCAO PUBLICADA NA RPI 2766 DE 09-01-2024 E CONSIDERANDO AUSENCIA DE MANIFESTACAO DENTRO DOS PRAZOS LEGAIS, INFORMO QUE CABE SER MANTIDA A EXTINCAO DA PATENTE E SEUS CERTIFICADOS, CONFORME O DISPOSTO NO ARTIGO 12, DA RESOLUCAO 113/2013.